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JPS6291225A - air purifier - Google Patents

air purifier

Info

Publication number
JPS6291225A
JPS6291225A JP60230977A JP23097785A JPS6291225A JP S6291225 A JPS6291225 A JP S6291225A JP 60230977 A JP60230977 A JP 60230977A JP 23097785 A JP23097785 A JP 23097785A JP S6291225 A JPS6291225 A JP S6291225A
Authority
JP
Japan
Prior art keywords
air
purifying agent
air purifying
gas
fiber paper
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Pending
Application number
JP60230977A
Other languages
Japanese (ja)
Inventor
Yoshiharu Kobayashi
小林 美春
Shozo Ichimura
市村 正三
Michinori Hashimoto
橋本 道憲
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Nippon Chemical Industrial Co Ltd
Original Assignee
Nippon Chemical Industrial Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Nippon Chemical Industrial Co Ltd filed Critical Nippon Chemical Industrial Co Ltd
Priority to JP60230977A priority Critical patent/JPS6291225A/en
Publication of JPS6291225A publication Critical patent/JPS6291225A/en
Pending legal-status Critical Current

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Abstract

PURPOSE:To offer an air-purifying agent with mechanical strength to be wrapped on the base of light weight by wrapping the soluble oxidizer on the mineral fiber paper. CONSTITUTION:after the mineral fiber paper made from mineral short fiber and made into desirable shape and size, for instance, such carriers as ceramic paper honeycomb of alumina silica family, is dipped in such soluble oxidizer as KMnO4 water solution and the like, the same is dried up to produce an air-purifying agent. The air-purifying agent thus produced is charged into the column and the like, and a wide scope of air pollutants or smelly substances such as H2S, SO2, NOx methyl mercaptan and the like are removed by passing the air containing pollutants or smelly substances through the said air-purifying agent charged in the column.

Description

【発明の詳細な説明】 [産業上の利用分野] 本発明は空気浄化剤に関し、さらに詳述すると大気汚染
物質又は悪臭物質を効率よく除去するために用いられる
薬剤を担持した無a譲維紙からなる空気浄化剤に関する
ものである。
DETAILED DESCRIPTION OF THE INVENTION [Industrial Application Field] The present invention relates to an air purifying agent, and more specifically, an a-free fiber paper carrying an agent used for efficiently removing air pollutants or malodorous substances. The present invention relates to an air purifying agent consisting of:

[従来の技術] 従来、工場、事務所、家庭等において、快適な環境をつ
くる一環として空気中に含有されている大気汚染物質又
は悪臭物質を除去して大気汚染の防止及び清浄化を計る
ために各種の方法が行われている。
[Conventional technology] Conventionally, in factories, offices, homes, etc., air pollutants or malodorous substances contained in the air are removed as part of creating a comfortable environment in order to prevent and purify the air. Various methods are being used.

例えば、過マンガン酸カリウムの如き酸化剤を活性アル
ミナ、ゼオライト等の所望の担体に含有せしめ、これを
球状9円柱状、うどん状又は破砕塊状などの成型体とし
て用いる空気浄化剤がある。
For example, there is an air purifying agent that contains an oxidizing agent such as potassium permanganate in a desired carrier such as activated alumina or zeolite, and uses this as a molded body such as a sphere, a cylinder, a udon shape, or a crushed lump.

また紙、布等に活性二酸化マンガンを担持したものが知
られている(特開昭48−71786号公報)。
Also known are paper, cloth, etc. that support activated manganese dioxide (Japanese Patent Application Laid-open No. 71786/1986).

一方1本発明者らは、上記のものを改良するものとして
過マンガン酸カリウムを含有した例えば活性アルミナま
たはゼオライトのハニカム成型体よりなる空気浄化剤を
開発した(特開昭60−108048号公報)。
On the other hand, the present inventors have developed an air purifying agent made of, for example, a honeycomb molded body of activated alumina or zeolite containing potassium permanganate as an improvement over the above-mentioned one (Japanese Patent Application Laid-open No. 108048/1983). .

他方、ハニカム成型体の空気浄化剤は、上記のほかに活
性炭で構成したハニカム成型体も知られている。
On the other hand, in addition to the above-mentioned air purifying agents for honeycomb molded bodies, honeycomb molded bodies made of activated carbon are also known.

[発明が解決しようとする問題点] 上記において球状1円柱状(うどん状)等の成型体の空
気浄化剤は、該成型体をステンレス、鉄等の金属あるい
はプラスチックの網よりなるフィルター、不織布等のフ
ィルターに充填して使用しているが、空気の通気抵抗が
高いため圧力損失が高く、小型のファンを使用した空気
浄化装置では十分な薬剤量を充填することが不可能であ
り、又該成型体は粉化し易く、強度が不足する欠点があ
る。
[Problems to be Solved by the Invention] In the above-mentioned air purifying agent in a molded body such as a sphere or a cylinder (udon shape), the molded body may be used as a filter made of a metal such as stainless steel or iron or a plastic mesh, a nonwoven fabric, etc. However, the pressure loss is high due to the high air ventilation resistance, and it is impossible to fill a sufficient amount of chemicals with an air purification device using a small fan. The molded product has the disadvantage of being easily powdered and lacking in strength.

一方、活性炭等の吸着作用を利用する方法として、活性
炭からなるハニカム成型体が知られているが、該ハニカ
ム成型体では大気汚染物質又は悪臭物質の中でNO、エ
チレン、ホルマリン等を全く除去できず、N)13 、
 H2S 、 S02等に対しては吸着能力が低く、活
性炭への吸着の飽和現象や脱着現象があり、父権〈稀薄
な濃度のガスに対しては吸着容量が小さい欠点がある。
On the other hand, a honeycomb molded body made of activated carbon is known as a method that utilizes the adsorption effect of activated carbon, but this honeycomb molded body cannot completely remove NO, ethylene, formalin, etc. among air pollutants or malodorous substances. zu, N) 13,
It has a low adsorption capacity for H2S, S02, etc., and there is a saturation phenomenon and desorption phenomenon of adsorption to activated carbon, and the adsorption capacity is small for gases with a dilute concentration.

他方、L記の欠点を改鮮すべく、本発明者らは先に、過
マンガン酸カリウム含有ハニカム成型体の空気浄化剤を
開発した。
On the other hand, in order to improve the shortcomings of item L, the present inventors have previously developed an air purifying agent for a honeycomb molded body containing potassium permanganate.

しかして、かかる空気浄化剤はいずれも機械的強度に劣
り、製造過程および使用上において、取扱いに慎重を要
すのみならず、大型にもなれば重量も結構無視できなく
なる。
However, all such air purifying agents have poor mechanical strength, and not only do they require careful handling during the manufacturing process and use, but their large size also makes their weight quite significant.

また、空気浄化性能は基材たるハニカム成型体の場合に
は、物性に大きく依存されるため、その基材の如何によ
って変動するので、再現性よくその品質保証することは
極めて重要なことである。
In addition, air purification performance is highly dependent on the physical properties of the honeycomb molded body used as the base material, so it varies depending on the type of base material, so it is extremely important to ensure its quality with good reproducibility. .

このようなことから本発明の目的は、機械的強度があり
、かつ軽量な基材に担持した空気浄化剤を提供すること
にある。
Therefore, an object of the present invention is to provide an air purifying agent supported on a mechanically strong and lightweight base material.

[問題点を解決するための手段] 本発明者等は、空気浄化剤において、その性能を左右す
る基材の研究を鋭意続けたところ、fil!111m紙
が予想外にすぐれていることを知見し本発明を完成した
[Means for Solving the Problems] The inventors of the present invention continued to earnestly research the base materials that affect the performance of air purifying agents, and found that fil! The present invention was completed after discovering that 111m paper was unexpectedly superior.

すなわち本発明は、無a譲維紙に溶解性酸化剤を有効成
分として担持してなることを特徴とする空気浄化剤にか
かる。
That is, the present invention relates to an air purifying agent characterized in that it is formed by supporting a soluble oxidizing agent as an active ingredient on a non-aluminum fiber paper.

本発明において担体となる黒磯繊維紙とは、天然又は合
成の無機質短繊維を抄紙してなる無機繊維紙をいい、無
機質繊維としては、例えば、アスベスト、ワラストナイ
トの如き天然魚*mm、ロックウール、スラグウール、
ガラスfa雄、シリカta雅、アルミナ繊維、シリカ・
アルミナ繊維、ムライトia維、ジルコニア繊維、炭素
繊維、ホウ素m維あるいは炭化珪素m維、窒化ホウ素繊
維等があげられ、これらは1種又は2種以上の配合で構
成されたam紙であっても差支えない。
The Kuroiso fiber paper used as a carrier in the present invention refers to an inorganic fiber paper made from natural or synthetic inorganic short fibers, and examples of inorganic fibers include asbestos, natural fish *mm such as wollastonite, and rock. wool, slag wool,
Glass FA Male, Silica TA Miyabi, Alumina Fiber, Silica・
Examples include alumina fibers, mullite IA fibers, zirconia fibers, carbon fibers, boron m-fibers or silicon carbide m-fibers, boron nitride fibers, etc., and even if these are am paper composed of one or more types of combinations. No problem.

かかるFa維紙は、抄紙の際に、天然又は合成の無機質
粉末をフィラーとして含有させたものであってもよく、
また、その紙の厚さは特に限定される必要はない。
Such Fa fiber paper may contain natural or synthetic inorganic powder as a filler during paper making,
Further, the thickness of the paper does not need to be particularly limited.

本発明において、無機繊維紙を担体として使用する場合
、所望の形状と大きさにして用いるが、空気浄化剤とし
て使用する態様に応じて設計されるものであるから形状
や大きさは特に限定される必要はない。
In the present invention, when inorganic fiber paper is used as a carrier, it is used in a desired shape and size, but the shape and size are not particularly limited because it is designed according to the mode of use as an air purifying agent. There is no need to

例えば、円形、正方形、直方形等の形状にて、単一紙状
のシート状、積層状、端層円筒状(バラムク−ヘン型)
あるいはハニカム状等の成型体などが所望により採用さ
れる。
For example, in the shape of a circle, square, rectangular parallelepiped, etc., in the form of a single paper sheet, laminated, end layer cylindrical (baramkuchen type)
Alternatively, a molded body such as a honeycomb shape may be employed as desired.

本発明では、特にハニカム成型体が好適なものとしてあ
げることができ、その断面形状は六角形、五角形、三角
形等の多角形、円形あるいは海綿状等のハニカム成型体
などいずれの場合であってもよく、所望により設計すれ
ばよい。
In the present invention, a honeycomb molded body is particularly suitable, and the cross-sectional shape of the honeycomb molded body may be polygonal such as hexagon, pentagon, or triangle, or circular or cavernous. It may be designed as desired.

次に、本発明において、上記無機繊維紙に担持する薬剤
は、溶解性酸化剤を有効成分とするものであるが、かか
る酸化剤としては、例えば過マンガン酸カリウム、鉄酸
カリウム、重クロム酸アルカリ、無水クロム酸1次亜ハ
ロゲン酸アルカリ。
Next, in the present invention, the drug supported on the inorganic fiber paper has a soluble oxidizing agent as an active ingredient, and such oxidizing agents include, for example, potassium permanganate, potassium ferrate, and dichromate. Alkali, chromic anhydride primary hypohalite alkali.

次亜ハロゲン酸カルシウム、過酸化ピロリンmカリウム
、過炭酸ソーダ、過炭酸ソーダ、過酸化カルシウムの如
き過酸化物等から選ばれた少なくとも1種又は2種以上
があげられ、これらのうち、過マンガン酸カリウムが特
に好ましい。
At least one or two or more peroxides selected from calcium hypohalite, pyrroline m potassium peroxide, sodium percarbonate, sodium percarbonate, calcium peroxide, etc., among which permanganese Potassium acid is particularly preferred.

かかる薬剤の無am維紙への担持量は、使用目的、薬剤
の種類、無機繊維紙の物性等によって異なるが、空気浄
化剤(乾燥基準)当り1〜20重量%の範囲であり、好
ましくは2〜15重量%であり、1重量%未満では除去
性能の寿命が短かくなり、又20重量%をこえると薬剤
の担持が困難となり、またハニカム成型体の細孔が塞が
れ除去効率が低下する傾向になり好ましくない。
The amount of such a drug supported on the non-am fiber paper varies depending on the purpose of use, the type of drug, the physical properties of the inorganic fiber paper, etc., but is preferably in the range of 1 to 20% by weight per air purifying agent (dry basis). If it is less than 1% by weight, the life of the removal performance will be shortened, and if it exceeds 20% by weight, it will be difficult to carry the drug, and the pores of the honeycomb molded body will be blocked, reducing the removal efficiency. This is not desirable as it tends to decrease.

なお、溶解性酸化剤を有効成分とするとは、担体に担持
させる場合、上記薬剤水溶液自体は勿論であるが、必要
に応じシリカゾル、アルミナゾルあるいは金属水酸化物
、金属珪酸塩などを薬剤水溶液に添加又は生成させる場
合も含むことを意味する。
Note that using a soluble oxidizing agent as an active ingredient means that when supporting it on a carrier, not only the above-mentioned aqueous drug solution itself, but also silica sol, alumina sol, metal hydroxide, metal silicate, etc., may be added to the aqueous drug solution as necessary. This also includes the case where it is generated.

本発明に係わる空気浄化剤は上記担体を特定の濃度の薬
剤水溶液、ゾル液又はスラリーに一定時間浸漬した後、
乾燥して薬剤を含浸せしめて担持することにより容易に
得ることができる。この際、薬剤水溶液の濃度は担体へ
の含浸効率を上げるためになるべく高濃度が好ましいが
、通常5〜20重量%の水溶液が好ましい。
The air purifying agent according to the present invention is prepared by immersing the carrier in an aqueous drug solution, sol, or slurry of a specific concentration for a certain period of time, and then
It can be easily obtained by drying, impregnating and supporting a drug. At this time, the concentration of the aqueous drug solution is preferably as high as possible in order to increase the efficiency of impregnating the carrier, but an aqueous solution of 5 to 20% by weight is usually preferred.

このようにして得られた本発明にかかる空気浄化剤を所
望の形状と大きさに調製した後カラム等に充填し、該カ
ラム内に大気汚染物質又は悪臭物質を含有する空気を通
過せしめることにより容易に空気の浄化を行うことがで
きる。
The air purifying agent according to the present invention thus obtained is prepared into a desired shape and size, and then packed into a column or the like, and air containing air pollutants or malodorous substances is passed through the column. Air can be easily purified.

本発明に係わる空気浄化剤は薬剤の酸化作用あるいは担
体の吸着作用により還元性ガス、酸化性ガスその他の広
範囲の大気汚染物質又は悪臭物質を除去することができ
る。該物質の具体例を示すと、NO,SO2,H2S、
 トリメチルアミン、トリエチルアミン等のアミン類、
硫化メチル等の硫化アルキル、 NH,、メチルメルカ
プタン等のメルカプタン類、ホルマリン等のアルデヒド
類、フェノール類、エチレン等の不飽和炭化水素等と下
水具、動物臭、N尿臭等の悪臭およびこれ等の混合物か
挙げられる。
The air purifying agent according to the present invention can remove reducing gases, oxidizing gases, and a wide range of other air pollutants or malodorous substances through the oxidizing action of the drug or the adsorption action of the carrier. Specific examples of the substance include NO, SO2, H2S,
Amines such as trimethylamine and triethylamine,
Alkyl sulfides such as methyl sulfide, NH, mercaptans such as methyl mercaptan, aldehydes such as formalin, phenols, unsaturated hydrocarbons such as ethylene, and bad odors such as sewage equipment, animal odor, N urine odor, etc. A mixture of

なお、Nしガスの除去の場合には、活性炭との併用が必
要である。
In addition, in the case of removing N gas, it is necessary to use activated carbon together.

[作 用] 本発明にかかる空気浄化剤に基づく空気汚染ガスの除去
の作用は、該ガスの種類や濃度によって、又浄化剤の物
性によって複雑であり、その詳細は不明であるが、基本
的には、空気中の水分を吸着して浄化剤中に保持された
少量の水分の介在か汚染ガスとの反応の律速段階となっ
て、分解か生ずるものと理解される。
[Function] The action of removing air polluting gas based on the air purifying agent of the present invention is complicated depending on the type and concentration of the gas and the physical properties of the purifying agent, and the details are unknown, but the basic principle is It is understood that decomposition occurs due to the presence of a small amount of moisture retained in the purifying agent by adsorbing moisture in the air, which becomes the rate-limiting step in the reaction with the pollutant gas.

このようなことから、本発明にかかる空気浄化剤は低湿
度の条件において充分水分保持能力のあるものが優れた
性能を発揮することができる。
For this reason, the air purifying agent according to the present invention can exhibit excellent performance if it has sufficient moisture retention ability under low humidity conditions.

[実施例] 次に、実施例及び比較例を示して、本発明をさらに具体
的に説明する。
[Example] Next, the present invention will be described in more detail by showing Examples and Comparative Examples.

実施例1 アルミナ・シリカ系のセラミックベーパーハニカムにチ
アス■社製、商品名ハニクルNoJ:119及びNo、
2813)の2種の担体、比較担体として活性アルミナ
ハニカム(任意アルミニウム製錬■社製:商品名5AH
−21)の合計3種の担体(いずれも大きさ2hmX 
20no+X 50mmの正四角柱)を50〜150 
g/  のKMnO4水溶液(液温60°C)に15分
間浸漬してKMnO,を担持した。
Example 1 Alumina-silica ceramic vapor honeycomb manufactured by Chias ■, product name Honeycle No. J: 119 and No.
2813), and activated alumina honeycomb (manufactured by Random Aluminum Smelting Company: trade name 5AH) as a comparison carrier.
-21) in total of three types of carriers (all with a size of 2hm
20no+X 50mm square prism) from 50 to 150
KMnO was supported by immersing it in a KMnO4 aqueous solution (liquid temperature 60°C) of 150 g/g for 15 minutes.

次いで乾燥して空気浄化剤を得、これをそれぞれ、22
ma+X 22+amX 70mmのカラムに充填して
空気浄化能を評価した。
Then, it was dried to obtain an air purifying agent, which was then dried to give 22
The air purification ability was evaluated by filling a ma+X 22+amX 70 mm column.

(t) 112s除去率の測定 カラム入口より、約5 ppmのH2Sガスで汚染した
空気(相対湿度60%、室温)を空間速度(SV値) 
25000および面風速(LV値)0.35テ通過せし
め、出口のH2Sを経時的にサンプリングし、ガスチッ
ク検知管(北洋産業■社製)  (4LL:感度0.0
5 ppm)で測定し、11.sの除去率を求めた。そ
の結果を第1表に示す。
(t) Air contaminated with approximately 5 ppm H2S gas (relative humidity 60%, room temperature) was collected at the space velocity (SV value) from the inlet of the 112s removal rate measurement column.
25,000 and a surface wind speed (LV value) of 0.35 Te, the H2S at the outlet was sampled over time, and a gastic detection tube (manufactured by Hokuyo Sangyo Co., Ltd.) (4LL: Sensitivity 0.0
5 ppm), 11. The removal rate of s was determined. The results are shown in Table 1.

(2) S02ガス除去率の測定 H2Sガスの代りにSO2ガス汚染空気を用いた以外は
H2Sガスの除去率の測定と全く同様の条件で測定した
。なお、S02ガスの測定はガスチック検知管(5La
)を用いた。その結果を第2表に示す。
(2) Measurement of S02 gas removal rate Measurement was carried out under exactly the same conditions as in the measurement of the H2S gas removal rate, except that air contaminated with SO2 gas was used instead of H2S gas. In addition, the measurement of S02 gas was carried out using a gastic detection tube (5La
) was used. The results are shown in Table 2.

(3) No、ガス除去率の測定 空気浄化剤A (KMJ104 3〜7重量%担持)の
後に活性炭ハニカム(20a+a+X 20ma+X 
50mm)を直列して充填したカラムにNOXで汚染し
た空気(室温。
(3) No. Measurement of gas removal rate Air purifier A (KMJ104 3 to 7% by weight supported) was followed by activated carbon honeycomb (20a+a+X 20ma+X
A column packed in series with NOx-contaminated air (room temperature).

相対湿度60%)ヲsv値25000−t’通過サセテ
、NOXガスの除去率を測定した。なお、NOx (N
O+NO2)ガスの測定はNOX メーターによる連続
化学発光法を用いた。その結果を第3表に示す。
The removal rate of NOX gas was measured at a relative humidity of 60% (relative humidity: 60%) and a sv value of 25,000-t'. Note that NOx (N
The continuous chemiluminescence method using a NOX meter was used to measure O+NO2) gas. The results are shown in Table 3.

第   3   表 実施例2 シリカ−アルミナを主成分とするセラミックベーパー(
厚さ1.s Imm)をロール状に巻き取り、直径30
■、長さ6cmの円柱にしたものを、150g/4のK
MnO4溶液に浸漬して、KMnO47,0重量%担持
した空気浄化剤を調製した。
Table 3 Example 2 Ceramic vapor mainly composed of silica-alumina (
Thickness 1. s Imm) into a roll and have a diameter of 30 mm.
■、150g/4 K made into a cylinder with a length of 6cm
An air purifying agent carrying 7.0% by weight of KMnO4 was prepared by immersing it in a MnO4 solution.

この空気?7.化剤を円形カラムに充填して入口より約
2 ppmのメチルメルカプタンで汚染した空気(室温
、相対湿度70%)をSv値tsoooで通過させて、
その除去率をみたところ、スタートより60分において
も除去率は97%以上を保持していた。なお、ガスの測
定はガスチック検知管を用いて測定した。
This air? 7. A circular column was filled with the oxidizing agent, and air (room temperature, relative humidity 70%) contaminated with about 2 ppm of methyl mercaptan was passed through the inlet with an Sv value of tsooo.
When looking at the removal rate, the removal rate remained at 97% or higher even 60 minutes after the start. The gas was measured using a gas detection tube.

実施例3 実施例2で用いたのと同じセラミ、:、クベーバーを短
冊状(2hmX 50mm)に切り、実施例2と同様に
してKMnO,7,:1重量%担持した空気浄化剤を調
製した。これをカラムに第一列は水平に、第二列はこれ
と直角になるように垂直に重ねて充填(各シート間は約
1a++sの間隙を保つ)して実施例1と同様にH,S
ガスで汚染した空気を通過させたところ、通過120分
後においてもH,Sガス除去率は実質100%であった
Example 3 The same ceramic cuber as used in Example 2 was cut into strips (2hm x 50 mm), and an air purifying agent carrying 1% by weight of KMnO, 7, : was prepared in the same manner as in Example 2. . Fill the columns with H, S
When air contaminated with gas was passed through the tube, the H,S gas removal rate was essentially 100% even after 120 minutes.

実施例4 実施例1で用いたセラミックベーパーハニカム(ハニク
ルNo、3:119 :ニチアス■社製)を重クロム酸
カリウム水溶液に浸漬してに2Cr20t  6.5重
量%担持した空気浄化剤を調製した。これを実施例1と
同様にカラムに充填してSO2ガスで汚染した空気を通
過せしめ、その60分後の除去率を経時的に測定したと
ころ、除去率98%以上を示し、実質的に汚染ガスを除
去することができた。
Example 4 An air purifying agent carrying 6.5% by weight of 2Cr20t was prepared by immersing the ceramic vapor honeycomb used in Example 1 (Honey No. 3:119, manufactured by Nichias Corporation) in an aqueous potassium dichromate solution. . This was packed into a column in the same manner as in Example 1, and the air contaminated with SO2 gas was passed through.The removal rate was measured over time after 60 minutes, and the removal rate was 98% or more, meaning that the air contaminated with SO2 gas was passed through. gas could be removed.

比較例1 KMnOa結晶17重量部、ゼオライト43重量部、ベ
ントナイト10重量部、珪酸カルシウム13重量部。
Comparative Example 1 17 parts by weight of KMnOa crystal, 43 parts by weight of zeolite, 10 parts by weight of bentonite, 13 parts by weight of calcium silicate.

消石灰13重量部、 5i0220重量部、コロイドシ
リカ16.5重量部および水82.5重量部からなる混
合物を充分に混練した後、押出成型機にて直径3mm、
長さ10m+sの円柱状に成型し、次いで110℃にて
乾燥して空気浄化剤を調製した。
After thoroughly kneading a mixture consisting of 13 parts by weight of slaked lime, 5i0220 parts by weight, 16.5 parts by weight of colloidal silica, and 82.5 parts by weight of water, it was molded into 3 mm diameter pieces using an extrusion molding machine.
It was molded into a cylindrical shape with a length of 10 m+s, and then dried at 110°C to prepare an air purifying agent.

このものを実施例1におけるH2Sガス汚染空気の測定
条件と全く同様な条件でH2Sガスの除去率の測定をし
たところ、第4表の結果が得られた。
When the H2S gas removal rate of this product was measured under exactly the same conditions as those used for measuring H2S gas-contaminated air in Example 1, the results shown in Table 4 were obtained.

第    4    表 実施例5および比較例2 実施例2で用いたと同じロール状円柱担体を50g#)
  KMnO4溶液に60℃で、15分間浸漬し1次い
で乾燥してKMnO42,1重量%担持した空気浄化剤
(A)を調製した。
Table 4 Example 5 and Comparative Example 2 50 g of the same rolled cylindrical carrier used in Example 2
An air purifying agent (A) carrying 1% by weight of KMnO4 was prepared by immersing it in a KMnO4 solution at 60°C for 15 minutes and then drying it.

他方、比較のため、ロール前の無aam維紙を508/
i’  KMnOa溶液および1重量%ゼラチン水溶液
との混合液に同様に浸漬した後、110°Cで乾燥後、
その全面に0.5重量%ホルムアルデヒド水溶液を均一
に噴霧してKMnO4を還元したのち、ロール状に巻き
とり、乾燥したものを空気浄化剤(B)とした。この2
種の空気浄化剤を、それぞれカラムに充填し、実施例1
と同様にして、SO2ガスで汚染した空気をカラムに通
過させて、その除去率を測定したところ、第5表の結果
が得られた。
On the other hand, for comparison, the non-aam fiber paper before rolling was 508/
i' After being similarly immersed in a mixture of a KMnOa solution and a 1 wt % gelatin aqueous solution, and dried at 110 °C,
After the KMnO4 was reduced by uniformly spraying a 0.5% by weight aqueous formaldehyde solution over the entire surface, it was wound up into a roll and dried, which was used as an air purifying agent (B). This 2
Example 1
In the same manner as above, when air contaminated with SO2 gas was passed through the column and the removal rate was measured, the results shown in Table 5 were obtained.

第    5    表 (数値は%) 実施例6 実施例1で調製したハニカム形の空気浄化剤(ハニクル
No、:l:+1!l )  (KMnO< 7重量%
担持)をカラムに充填し、1 ppm  11.3ガス
で汚染した常温かつ大気湿度(相対湿度60%)にある
空気をSV値2500で8000時ni1通過させて1
通過後のガスを経時的にサンプリングしてガスクロ分析
(感度0.02ppb ) L/てガスの除去率を監視
したところ、8000時間に至うてもなお11□Sガス
の除去率は99%以上であった。
Table 5 (values are %) Example 6 Honeycomb-shaped air purifying agent prepared in Example 1 (Honey No.:l:+1!l) (KMnO<7% by weight
The column was packed with 1 ppm 11.3 gas and air at room temperature and atmospheric humidity (relative humidity 60%) was passed through the column at 8000 hours with an SV value of 2500.
The gas removal rate was monitored by gas chromatography analysis (sensitivity 0.02 ppb) L/L after passing through the gas over time, and the removal rate of 11□S gas was still over 99% even after 8000 hours. Met.

[発明の効果] 本発明にかかる空気浄化剤は、例えば従来のハニカム成
型体の空気浄化剤に比して軽量かつ機械的強度が高いの
で信頼性が向上し、また、空気浄化能も一定のレベルで
再現性よく発揮することができる。
[Effects of the Invention] The air purifying agent according to the present invention is lighter and has higher mechanical strength than, for example, conventional honeycomb molded air purifying agents, so reliability is improved, and air purifying ability is also maintained at a certain level. It can be demonstrated with good reproducibility at various levels.

即ち、本発明にかかる空気浄化剤は軽量かつ機械的強度
があるため、成形が容易なところから、フィルター、エ
アコン、クーラー等の所望の機器に組み込むことができ
、各種の機器、又は装置等あるいは環境に基因する悪臭
又は有害ガスを効果的に除去して空気を清浄化すること
ができる。特にハニカム体にしたものは、圧力損失か少
ないので、風量が少量でも充分機能し長時間、使用に酎
えることができる。
That is, since the air purifying agent according to the present invention is lightweight and has mechanical strength, it can be easily molded and can be incorporated into desired equipment such as filters, air conditioners, and coolers. Air can be purified by effectively removing bad odors or harmful gases originating from the environment. In particular, the honeycomb body has a low pressure loss, so it can function satisfactorily even with a small amount of airflow and can be used for a long time.

Claims (4)

【特許請求の範囲】[Claims] (1)無機繊維紙に溶解性酸化剤を有効成分として担持
してなることを特徴とする空気浄化剤。
(1) An air purifying agent comprising an inorganic fiber paper supporting a soluble oxidizing agent as an active ingredient.
(2)無機繊維紙がハニカム成型体に構成されたもので
ある特許請求の範囲第1項記載の空気浄化剤。
(2) The air purifying agent according to claim 1, wherein the inorganic fiber paper is formed into a honeycomb molded body.
(3)溶解性酸化剤が過マンガン酸カリウム、クロム酸
塩又は鉄酸カリウムから選ばれた少なくとも1種又は2
種以上である特許請求の範囲第1項記載の空気浄化剤。
(3) The soluble oxidizing agent is at least one or two selected from potassium permanganate, chromate, or potassium ferrate.
The air purifying agent according to claim 1, which is more than 1 species.
(4)溶解性酸化剤は空気浄化剤(乾燥基準)当り1〜
20重量%無機繊維紙に担持したものである特許請求の
範囲第1項又は第3項記載の空気浄化剤。
(4) Soluble oxidizing agent: 1 to 1 per air purifying agent (dry basis)
The air purifying agent according to claim 1 or 3, which is supported on 20% by weight inorganic fiber paper.
JP60230977A 1985-10-18 1985-10-18 air purifier Pending JPS6291225A (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
JP60230977A JPS6291225A (en) 1985-10-18 1985-10-18 air purifier

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
JP60230977A JPS6291225A (en) 1985-10-18 1985-10-18 air purifier

Publications (1)

Publication Number Publication Date
JPS6291225A true JPS6291225A (en) 1987-04-25

Family

ID=16916287

Family Applications (1)

Application Number Title Priority Date Filing Date
JP60230977A Pending JPS6291225A (en) 1985-10-18 1985-10-18 air purifier

Country Status (1)

Country Link
JP (1) JPS6291225A (en)

Cited By (10)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0346342U (en) * 1989-09-13 1991-04-30
KR100452148B1 (en) * 2001-04-10 2004-10-12 (주) 솔리브 Elemination of Tabacco Injurious Gas by Adsorbent
KR100456185B1 (en) * 2001-07-25 2004-11-10 주식회사 얼라이브텍 Eliminator For Removing Harmful Gases In Flue Gases And Method For Removing The Sames Thereby
JP2008093490A (en) * 2006-06-28 2008-04-24 National Institute For Minamata Disease Ministry Of The Environment Sulfur oxide adsorption method
WO2008112657A1 (en) * 2007-03-09 2008-09-18 Battelle Memorial Institute Ferrate(vi)-containing compositions and methods of using ferrate(vi)
US8034253B2 (en) 2004-11-12 2011-10-11 Battelle Memorial Insitute Decontaminant
WO2012018870A1 (en) * 2010-08-02 2012-02-09 Battle Memorial Institute Co2 sorbent composition with o2 co-generation
US8449756B2 (en) 2004-01-16 2013-05-28 Battelle Memorial Institute Method for producing ferrate (V) and/or (VI)
US8722147B2 (en) 2008-10-17 2014-05-13 Battelle Memorial Institute Corrosion resistant primer coating
US8944048B2 (en) 2008-03-26 2015-02-03 Battelle Memorial Institute Apparatus and methods of providing diatomic oxygen (O2) using ferrate(VI)-containing compositions

Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5652021B2 (en) * 1976-04-23 1981-12-09
JPS57102221A (en) * 1980-12-16 1982-06-25 Toshimi Kuma Production of element for deodorization
JPS5881425A (en) * 1981-11-11 1983-05-16 Matsushita Electric Ind Co Ltd Apparatus for removing ozone
JPS60108048A (en) * 1983-11-17 1985-06-13 日本化学工業株式会社 Air purifying agent

Patent Citations (4)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPS5652021B2 (en) * 1976-04-23 1981-12-09
JPS57102221A (en) * 1980-12-16 1982-06-25 Toshimi Kuma Production of element for deodorization
JPS5881425A (en) * 1981-11-11 1983-05-16 Matsushita Electric Ind Co Ltd Apparatus for removing ozone
JPS60108048A (en) * 1983-11-17 1985-06-13 日本化学工業株式会社 Air purifying agent

Cited By (11)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
JPH0346342U (en) * 1989-09-13 1991-04-30
KR100452148B1 (en) * 2001-04-10 2004-10-12 (주) 솔리브 Elemination of Tabacco Injurious Gas by Adsorbent
KR100456185B1 (en) * 2001-07-25 2004-11-10 주식회사 얼라이브텍 Eliminator For Removing Harmful Gases In Flue Gases And Method For Removing The Sames Thereby
US8449756B2 (en) 2004-01-16 2013-05-28 Battelle Memorial Institute Method for producing ferrate (V) and/or (VI)
US8034253B2 (en) 2004-11-12 2011-10-11 Battelle Memorial Insitute Decontaminant
JP2008093490A (en) * 2006-06-28 2008-04-24 National Institute For Minamata Disease Ministry Of The Environment Sulfur oxide adsorption method
WO2008112657A1 (en) * 2007-03-09 2008-09-18 Battelle Memorial Institute Ferrate(vi)-containing compositions and methods of using ferrate(vi)
US8663607B2 (en) 2007-03-09 2014-03-04 Battelle Memorial Institute Ferrate(VI)-containing compositions and methods of using ferrate(VI)
US8944048B2 (en) 2008-03-26 2015-02-03 Battelle Memorial Institute Apparatus and methods of providing diatomic oxygen (O2) using ferrate(VI)-containing compositions
US8722147B2 (en) 2008-10-17 2014-05-13 Battelle Memorial Institute Corrosion resistant primer coating
WO2012018870A1 (en) * 2010-08-02 2012-02-09 Battle Memorial Institute Co2 sorbent composition with o2 co-generation

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